2009
DOI: 10.1016/j.expthermflusci.2008.11.004
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Experimental investigation of turbulence modulation in particle-laden coaxial jets by Phase Doppler Anemometry

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Cited by 19 publications
(8 citation statements)
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“…The weaker vortices will have little effect on the particles. However, if the Stokes number is much greater than 1, the momentum response time of the discrete phase is much greater than that of the time constant of the flow field and the discrete phase flow will pass through the turbulent vortices, although individual particles will show slight variations in their velocities because of a very small momentum exchange with the vorticies, as found by Mostafa et al [5] and Mergheni et al [6]. In this case, there will be transfer of turbulent kinetic energy to the fluid from the particles because the particles will create turbulent motion on a scale about their diameter, as suggested by Gore and Crowe [7].…”
Section: Introductionmentioning
confidence: 81%
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“…The weaker vortices will have little effect on the particles. However, if the Stokes number is much greater than 1, the momentum response time of the discrete phase is much greater than that of the time constant of the flow field and the discrete phase flow will pass through the turbulent vortices, although individual particles will show slight variations in their velocities because of a very small momentum exchange with the vorticies, as found by Mostafa et al [5] and Mergheni et al [6]. In this case, there will be transfer of turbulent kinetic energy to the fluid from the particles because the particles will create turbulent motion on a scale about their diameter, as suggested by Gore and Crowe [7].…”
Section: Introductionmentioning
confidence: 81%
“…Mergheni et al [6] investigated coaxial jet flows with 102-212 µm diameter glass spheres introduced in the central jet with two annular to central jet velocity ratios, 0.2 and 1.3. In the case of the slower central jet, the onset of a single peak mean axial velocity profile, indicating jet merging, was slightly beyond 10 nozzle diameters, the last profile reported.…”
Section: Introductionmentioning
confidence: 99%
“…Vreman et al (2007) showed that there is another suppressing mechanism in inhomogeneous flows: the non-uniform relative velocity of the phases created because particles slip at the wall, collide, and slowly react with the continuous phase. Mergheni et al (2009) found that, near the injector at low Reynolds number, the presence of the particles dampens the gas-phase turbulence, while at higher Reynolds number, the gas-phase turbulence and the velocity fluctuation of particleladen jets are increased. Anand and Jenny (2009) presented a unified probability density function formulation for capturing the phenomena of turbulence modification of the continuous phase due to the dispersed phase turbulence, and gave the influence of gravity on the decay of the continuous phase Reynolds stresses.…”
Section: Introductionmentioning
confidence: 96%
“…Nezu and Azuma [6] utilized PTV method to simultaneously measure the velocities of solid and liquid phases in an open channel flow, and substantial turbulence enhancement was observed in the vicinity of the surface due to the particle movement. Mergheni et al [7] carried out experimental study on a vertical coaxial jet by PDA, from which the existence of particles was observed to reduce the velocity gradient in the shear layer, causing a decrease in turbulence intensity. In the recent simulation studies [8,9], the turbulence enhancement by large particles, as well as the turbulence attenuation by small particles have both been successfully predicted in a unified model by appropriate numerical settings.…”
Section: Introductionmentioning
confidence: 97%